US10442709B2 - Selectively permeable graphene oxide membrane - Google Patents

Selectively permeable graphene oxide membrane Download PDF

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US10442709B2
US10442709B2 US15/380,797 US201615380797A US10442709B2 US 10442709 B2 US10442709 B2 US 10442709B2 US 201615380797 A US201615380797 A US 201615380797A US 10442709 B2 US10442709 B2 US 10442709B2
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membrane
graphene oxide
cross
layer
mpd
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US20170174537A1 (en
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Shijun Zheng
Isamu Kitahara
Makoto Kobuke
Peng Wang
Craig Roger Bartels
Yuji Yamashiro
Masahiko Hirose
Shunsuke Noumi
Weiping Lin
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Nitto Denko Corp
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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0002—Organic membrane manufacture
    • B01D67/0006—Organic membrane manufacture by chemical reactions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0039—Inorganic membrane manufacture
    • B01D67/0041—Inorganic membrane manufacture by agglomeration of particles in the dry state
    • B01D67/00416—Inorganic membrane manufacture by agglomeration of particles in the dry state by deposition by filtration through a support or base layer
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0039—Inorganic membrane manufacture
    • B01D67/0044—Inorganic membrane manufacture by chemical reaction
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0079—Manufacture of membranes comprising organic and inorganic components
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0079—Manufacture of membranes comprising organic and inorganic components
    • B01D67/00791—Different components in separate layers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0079—Manufacture of membranes comprising organic and inorganic components
    • B01D67/00793—Dispersing a component, e.g. as particles or powder, in another component
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0081—After-treatment of organic or inorganic membranes
    • B01D67/0083—Thermal after-treatment
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/08—Hollow fibre membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/10—Supported membranes; Membrane supports
    • B01D69/107—Organic support material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12—Composite membranes; Ultra-thin membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12—Composite membranes; Ultra-thin membranes
    • B01D69/1213—Laminated layers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12—Composite membranes; Ultra-thin membranes
    • B01D69/1214—Chemically bonded layers, e.g. cross-linking
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12—Composite membranes; Ultra-thin membranes
    • B01D69/1216—Three or more layers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12—Composite membranes; Ultra-thin membranes
    • B01D69/125—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12—Composite membranes; Ultra-thin membranes
    • B01D69/125—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction
    • B01D69/1251—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction by interfacial polymerisation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/14—Dynamic membranes
    • B01D69/141—Heterogeneous membranes, e.g. containing dispersed material; Mixed matrix membranes
    • B01D69/148—Organic/inorganic mixed matrix membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/02—Inorganic material
    • B01D71/021—Carbon
    • B01D71/0211—Graphene or derivates thereof
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/02—Inorganic material
    • B01D71/024—Oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/38—Polyalkenylalcohols; Polyalkenylesters; Polyalkenylethers; Polyalkenylaldehydes; Polyalkenylketones; Polyalkenylacetals; Polyalkenylketals
    • B01D71/381—Polyvinylalcohol
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2323/00—Details relating to membrane preparation
    • B01D2323/30—Cross-linking
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2325/00—Details relating to properties of membranes
    • B01D2325/04—Characteristic thickness
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2325/00—Details relating to properties of membranes
    • B01D2325/36—Hydrophilic membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/025—Reverse osmosis; Hyperfiltration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02—Hollow fibre modules
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/56—Polyamides, e.g. polyester-amides
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124—Water desalination
    • Y02A20/131—Reverse-osmosis

Definitions

  • the present embodiments are related to polymeric membranes, including membranes comprising graphene materials for uses such as water treatment, desalination of saline water, or water removal.
  • RO membranes Due to the increase of human population and water consumption coupled with limited freshwater resources on earth, technologies such as seawater desalination and water treatment/recycle to provide safe and fresh water have become more important to our society.
  • the desalination process using reverse osmosis (RO) membrane is the leading technology for producing fresh water from saline water.
  • Most of current commercial RO membranes adopt a thin-film composite (TFC) configuration consisting of a thin aromatic polyamide selective layer on top of a microporous substrate; typically a polysulfone membrane on non-woven polyester.
  • TFC thin-film composite
  • these RO membranes can provide excellent salt rejection rate, higher water flux; thinner and more hydrophilic membranes are still desired to further improve energy efficiency of RO. Therefore, new membrane materials and synthetic methods are in high demand to achieve the desired properties as described above.
  • the GO membrane composition may be prepared by using a water soluble cross-linker.
  • the water soluble cross-linker may be one that is compatible with the polyamide coating of a reverse osmosis membrane. Methods of efficiently and economically making these GO membrane compositions are also described. Water can be used as a solvent in preparing these GO membrane compositions, which makes the membrane preparation process more environmentally friendly and more cost effective.
  • cross-linker is interchangeable with the term “crosslinker”.
  • Some embodiments include a selectively permeable polymeric membrane, such as a membrane comprising the high water flux GO membrane composition, for water treatment and desalination of saline water.
  • Some embodiments include a GO-MPD (meta-phenylenediamine) membrane comprising a porous substrate, and a graphene oxide layer comprising an optionally substituted cross-linked graphene oxide in fluid communication with the porous substrate, wherein the optionally substituted cross-linked graphene oxide comprises an optionally substituted graphene oxide and a cross-linkage represented by Formula I or Formula 1M:
  • the resulting membrane containing GO-MPD composite as described herein further comprises a salt rejection layer, and/or a protection layer.
  • cross-linked is interchangeable with the term “crosslinked”
  • cross-linkage is interchangeable with the term “crosslinkage”.
  • Some embodiments include a method of dehydrating an unprocessed fluid comprising exposing the unprocessed fluid to the above described membranes, or removing a solute, such as desalination, from an unprocessed solution comprising exposing or passing the unprocessed solution to the aforementioned membranes.
  • passing the unprocessed solution through the membrane is achieved by applying a pressure gradient across the membrane.
  • Some embodiments include a method of making a membrane, such as dehydration membrane or desalination membrane, comprising mixing an optionally substituted graphene oxide (GO) and a cross-linker, such as an optionally substituted meta-phenylenediamine to get an aqueous solution, followed by resting to get a coating mixture and applying the coating mixture to a substrate, and curing the GO and the cross-linker on the substrate until they are covalently bonded.
  • Some embodiments include separately applying the optionally substituted GO aqueous solution and an optionally substituted meta-phenylenediamine cross-linker aqueous solution to a substrate followed by the same process and conditions of curing until they are covalently bonded.
  • the method further comprising applying a salt rejection layer, and/or a protection layer.
  • FIG. 1 is a diagram showing the graphene oxide layers of a GO-MPD membrane.
  • FIGS. 2A-2B is a depiction of two possible embodiments of membranes without a salt rejection layer or a protective coating.
  • FIGS. 3A-3B is a depiction of two possible embodiments of membranes without a salt rejection layer but with a protective coating.
  • FIGS. 4A-4B is a depiction of two possible embodiments of membranes with a salt rejection layer but without a protective coating.
  • FIGS. 5A-5B is a depiction of two possible embodiments of membranes with a salt rejection layer and a protective coating.
  • FIG. 6 is a depiction of a possible embodiment for the method for making a membrane—Layer-by-Layer Method.
  • FIG. 7 is a depiction of a possible embodiment for the method of making a membrane—Filter Method
  • FIG. 8 is a depiction of a possible embodiment for the method of making a membrane—Mixture Coating Method.
  • FIGS. 9A-9B shows SEM data of a membrane showing a substrate, the GO-MPD layer, and a protective coating (resin).
  • FIG. 10 is a plot of XRD data for GO and GO-MPD each on a glass slide with control plots for each glass slide.
  • FIG. 11 is a plot showing the infrared (IR) spectra comparison of GO and GO-MPD.
  • FIG. 12 is a diagram depicting the experimental setup for the water vapor permeability and gas leakage testing.
  • a selectively permeable membrane includes a membrane that is relatively permeable for one material and relatively impermeable for another material.
  • a membrane may be relatively permeable to water or water vapor and relatively impermeable to organic liquids or oxygen or nitrogen gas.
  • the term “rest,” “resting,” or “rested” includes the act of leaving a solution stand undisturbed at room temperature and atmospheric pressure for a specific duration of time.
  • a compound or a chemical structure such as graphene oxide or phenylenediamine
  • “optionally substituted” it includes a compound or a chemical structure that either has no substituents (i.e., unsubstituted), or has one or more substituents (i.e., substituted).
  • substituted has the broadest meaning known in the art, and includes a moiety that replaces one or more hydrogen atoms attached to a parent compound or structure.
  • a substituent may be any type of group that may be present on a structure of an organic compound, which may have a molecular weight (e.g., the sum of the atomic masses of the atoms of the substituent) of 15-50 g/mol, 15-100 g/mol, 15-150 g/mol, 15-200 g/mol, 15-300 g/mol, or 15-500 g/mol.
  • a molecular weight e.g., the sum of the atomic masses of the atoms of the substituent
  • a substituent comprises, or consists of: 0-30, 0-20, 0-10, or 0-5 carbon atoms; and 0-30, 0-20, 0-10, or 0-5 heteroatoms, wherein each heteroatom may independently be: N, O, S, Si, F, Cl, Br, or I; provided that the substituent includes one C, N, O, S, Si, F, Cl, Br, or I atom.
  • substituents include, but are not limited to, alkyl, alkenyl, alkynyl, heteroalkyl, heteroalkenyl, heteroalkynyl, aryl, heteroaryl, hydroxy, alkoxy, aryloxy, acyl, acyloxy, alkylcarboxylate, thiol, alkylthio, cyano, halo, thiocarbonyl, O-carbamyl, N-carbamyl, O-thiocarbamyl, N-thiocarbamyl, C-amido, N-amido, S-sulfonamido, N-sulfonamido, isocyanato, thiocyanato, isothiocyanato, nitro, silyl, sulfenyl, sulfinyl, sulfonyl, haloalkyl, haloalkoxyl, trihalomethanesulfonyl, trihalome
  • molecular weight is used with respect to a moiety or part of a molecule to indicate the sum of the atomic masses of the atoms in the moiety or part of a molecule, even though it may not be a complete molecule.
  • fluid includes any substance that continually deforms, or flows, under an applied shear stress.
  • fluids include Newtonian and/or non-Newtonian fluids.
  • examples of Newtonian can be gases, liquids, and/or plasmas.
  • non-Newtonian fluids can be plastic solids (e.g., corn starch aqueous solution, toothpaste).
  • fluid communication means that a fluid can pass through a first component and travel to and through a second component or more components regardless of whether they are in physical communication or the order of arrangement.
  • the present disclosure relates to water separation membranes where a highly hydrophilic membrane with low organic compound permeability and high mechanical and chemical stability may be useful to support the polyamide salt rejection layer in a reverse osmosis (RO) membrane.
  • This membrane material may be suitable for solute removal from an unprocessed fluid, such as desalination from saline water, or purifying drinking water, such as waste water treatment.
  • This membrane material may be suitable in the dehydration or water/water vapor removal from an unprocessed fluid.
  • Some selective water permeable membranes described herein are GO-MPD membranes having a high water flux, which may improve the energy efficiency of RO membranes and improve water recovery/separation efficiency.
  • the water permeable GO-MPD membrane comprises an optionally substituted graphene oxide (GO) crosslinked with an optionally substituted arylenediamine, such as an optionally substituted water soluble meta-phenylenediamine (MPD).
  • GO graphene oxide
  • MPD water soluble meta-phenylenediamine
  • the selectively permeable membrane further comprises a porous substrate or support, such as a porous support comprising a polymer or hollow fibers.
  • a porous substrate or support such as a porous support comprising a polymer or hollow fibers.
  • the GO-MPD layer or membrane is disposed on the porous support.
  • the GO-MPD layer or membrane may further be in fluid communication with the substrate. Additional optional layers may also be included such as a salt rejection layer disposed on the GO-MPD layer, a protective layer, and etc.
  • the protective layer can comprise a hydrophilic polymer.
  • the fluid passing through the membrane travels through all the components regardless of whether they are in physical communication or the order of arrangement.
  • a substrate may be any suitable material and in any suitable form upon which a layer, such as a layers of a GO-MBD membrane, may be deposited or disposed.
  • the substrate may comprise a porous material, such as a polymer or a hollow fiber.
  • the polymer may be polyethylene (PE), polypropalene (PP), polysulfone (PSF), polyether sulfone (PES), polyvinylidene fluoride (PVDF), polyamide (Nylon), polyimide (PI), and/or mixtures thereof.
  • the polymer may be polysulfone.
  • the porous material may comprise a polysulfone based ultrafiltration membrane.
  • the porous material may comprise hollow fibers.
  • the hollow fibers may be casted or extruded.
  • the hollow fibers may be made, for example, as described in U.S. Pat. Nos. 4,900,626; 6,805,730 and U. S. Patent Application Publication No. 2015/0165389, which are incorporated by reference for their disclosure related to methods of preparing hollow fibers.
  • Some membranes further comprise a salt rejection layer, e.g. disposed on the GO-MPD layer.
  • a salt rejection layer may comprise any material that is suitable for preventing the passage of salts.
  • Some salt rejection layers comprise a polymer, such as a polyamide or a mixture of polyamides.
  • the polyamide can be a polyamide made from an amine (e.g. meta-phenylenediamine, para-phenylenediamine, ortho-phenylenediamine, piperazine, polyethylenimine, polyvinylamine, or the like) and an acyl chloride (e.g. trimesoyl chloride, isophthaloyl chloride, or the like).
  • the amine can be meta-phenylenediamine.
  • the acyl chloride can be trimesoyl chloride.
  • the polyamide can be made from a meta-phenylenediamine and a trimesoyl chloride (e.g. by polymerization of meta-phenylenediamine and/or trimesoyl chloride).
  • having the salt rejection layer include the same type of structural feature as the GO-MPD membrane (also made from MPD) upon which it is disposed can avoid adverse interaction between the two layers.
  • some membranes may further comprise a protective coating.
  • the protective coating can be disposed on top of the membrane to protect it from the environment.
  • the protective coating may have any composition suitable for protecting a membrane from the environment, Many polymers are suitable for use in a protective coating such as one or a mixture of hydrophilic polymers, e.g.
  • polyvinyl alcohol PVA
  • polyvinyl pyrrolidone PVP
  • polyethylene glycol PEG
  • polyethylene oxide PEO
  • polyoxyethylene POE
  • PAA polyacrylic acid
  • PMMA polymethacrylic acid
  • PAM polyacrylamide
  • PEI polyethylenimine
  • PES polyethersulfone
  • MC methyl cellulose
  • chitosan poly (allylamine hydrochloride) (PAH) and poly (sodium 4-styrene sulfonate) (PSS), and any combinations thereof.
  • the protective coating can comprise PVA.
  • a membrane 100 without a salt rejection layer may be configured as shown in FIGS. 2A, 2B, 3A and 3B .
  • the membrane 100 can comprise at least a substrate 120 and a cross-linked graphene material layer 110 .
  • the membrane may further comprise a protective coating, 140 .
  • the membrane can be without a protective coating.
  • the cross-linked graphene material layer, 110 can be initially constructed to have alternating layers of graphene oxide, 111 , and cross-linker, 112 .
  • the cross-linked graphene material layer may comprise a single layer of a mixture of graphene oxide and cross-linker, 113 .
  • the substrate may be sandwiched between two aforementioned membranes.
  • the membrane can allow the passage of water and/or water vapor, but resists the passage of gases.
  • the membrane may provide a means of removal of water from a control volume by allowing water vapor to pass through but excluding the passage of other gases; resulting in passive dehydration.
  • the membrane can be used to remove water or water vapor from a control volume while hindering the passage of solutes or other fluids, such as gases.
  • a membrane may be disposed between or separate a fluidly communicated first fluid reservoir and a second fluid reservoir.
  • the first reservoir may contain a feed fluid upstream and/or at the membrane.
  • the fluid upstream can comprise a gas and water vapor.
  • the second reservoir may contain a processed fluid downstream and/or at the membrane.
  • the fluid downstream can have less humidity than that of the first reservoir.
  • the membrane selectively allows water or water vapor to pass through while resisting the passage of gas, solute, or liquid material from passing through.
  • the membrane may provide a filter to selectively remove solute and/or suspended contaminants from feed fluid.
  • the membrane has a desired flow rate.
  • the membrane may comprise ultrafiltration material.
  • the membrane can exhibit a water vapor permeability of about 15-100 ⁇ g ⁇ m ⁇ 2 ⁇ s ⁇ 1 ⁇ Pa ⁇ 1 , about 20-90 ⁇ g ⁇ m ⁇ 2 ⁇ s ⁇ 1 ⁇ Pa ⁇ 1 about 25-90 ⁇ g ⁇ m ⁇ 2 ⁇ s ⁇ 1 ⁇ Pa ⁇ 1 about 30-60 ⁇ g ⁇ m ⁇ 2 ⁇ s ⁇ 1 ⁇ Pa ⁇ 1 , about 30-40 ⁇ g ⁇ m ⁇ 2 ⁇ s ⁇ 1 ⁇ Pa ⁇ 1 , about 40-60 ⁇ g ⁇ m ⁇ 2 ⁇ s ⁇ 1 ⁇ Pa ⁇ 1 , about 40-50 ⁇ g ⁇ m ⁇ 2 ⁇ s ⁇ 1 ⁇ Pa ⁇ 1 , or about 50-60 ⁇ g ⁇ m ⁇ 2 ⁇ s ⁇ 1 ⁇ Pa ⁇ 1 .
  • the membrane can also have a maximum N 2 gas leakage rate of about 1000 cc/min, about 500 cc/min, about 100 cc/min, about 40 cc/min, about 25 cc/min, about 5 cc/min, less than 10 cc/min, or less than 5 cc/min.
  • a membrane 200 comprising a salt rejection layer 130 may be configured as shown in FIGS. 4A, 4B, 5A, and 5B .
  • the membrane 200 can comprise at least a substrate 120 a cross-linked graphene material layer 110 and a salt rejection layer 130 .
  • the salt rejection layer 130 may be disposed on top of the cross-linked graphene material layer 110 .
  • the membrane may further comprise a protective coating, 140 , wherein the protective coating can protect the components of the membrane from harsh environments.
  • the membrane can be without a protective coating.
  • the cross-linked graphene material layer 110 may be initially constructed to have an alternating layer of graphene material 111 and cross-linker 112 .
  • the cross-linked graphene material layer may comprise a single layer of a mixture of graphene material and cross-linker 113 .
  • the substrate may be sandwiched between two layers comprising GO-MPD.
  • the membrane selectively allows water or water vapor to pass through while keeping gas, solute, or liquid material from passing through.
  • the membrane may provide a durable desalination system that can be selectively permeable to water, and less permeable to salts.
  • the membrane may provide a durable reverse osmosis system that may effectively filter saline water, polluted water or feed fluids.
  • the membrane exhibits a normalized volumetric water flow rate of about 10-1000 gal ⁇ ft ⁇ 2 ⁇ day ⁇ 1 ⁇ bar ⁇ 1 ; about 20-750 gal ⁇ ft ⁇ 2 ⁇ day ⁇ 1 ⁇ bar ⁇ 1 ; about 100-500 gal ⁇ ft ⁇ 2 ⁇ day ⁇ 1 ⁇ bar ⁇ 1 ; about 200-400 gal ⁇ ft ⁇ 2 ⁇ day ⁇ 1 ⁇ bar ⁇ 1 , at least about 10 gal ⁇ ft ⁇ 2 ⁇ day ⁇ 1 ⁇ bar ⁇ 1 , about 20 gal ⁇ ft 2 ⁇ day ⁇ 1 ⁇ bar ⁇ 1 , about 100 gal ⁇ ft ⁇ 1 ⁇ day ⁇ 1 ⁇ bar ⁇ 1 , about 200 gal ⁇ ft 2 ⁇ day ⁇ 1 ⁇ bar ⁇ 1 or a normalized volumetric water flow rate in a range bounded by any of these values.
  • the cross-linked graphene oxide layer may have an average pore size or fluid passageway of an average diameter of about 0.01 ⁇ m (10 nm) to about 0.1 ⁇ m (100 nm), and/or about 0.01 ⁇ m (10 nm) to about 0.05 ⁇ m (50 nm).
  • a membrane may be a selectively permeable.
  • the membrane may be an osmosis membrane.
  • the membrane may be a water separation membrane.
  • a water permeable- and/or solute impermeable membrane containing graphene material, such as graphene oxide may provide desired selective gas, liquid, and/or vapor permeability resistance.
  • the membrane may be a reverse osmosis (RO) membrane.
  • the selectively permeable membrane may comprise multiple layers, wherein at least one layer contains graphene material.
  • the membranes described herein have a cross-linked optionally substituted graphene oxide.
  • These optionally substituted cross-linked graphene oxides include an optionally substituted graphene that is cross-linked with a water-soluble cross-linkage, or which are a product cross-linking graphene oxide with a water-soluble cross-linking agent.
  • cross-linking is interchangeable with the term “crosslinking”.
  • Graphene materials have many attractive properties, such as a 2-dimensional sheet-like structure with extraordinary high mechanical strength and nanometer scale thickness.
  • the graphene oxide (GO) an exfoliated oxidation of graphite, can be mass produced at low cost. With its high degree of oxidation, graphene oxide has high water permeability and also exhibits versatility to be functionalized by many functional groups, such as amines or alcohols to form various membrane structures. Unlike traditional membranes, where the water is transported through the pores of the material, in graphene oxide membranes the transportation of water can be between the interlayer spaces. Graphene oxide's capillary effect can result in long water slip lengths that offer fast water transportation rate. Additionally, the membrane's selectivity and water flux can be controlled by adjusting the interlayer distance of graphene sheets.
  • Layered GO membranes with lamellar structure can be fabricated by vacuum filtration process of GO aqueous solution, but may be highly susceptible to be dispersed in aqueous environment under high flux. To solve this issue, the GO sheets can be cross-linked firmly to withstand the water flux while keeping the lamellar structure.
  • the optionally substituted graphene oxide may be in the form of sheets, planes or flakes.
  • the graphene material may have a surface area of about 100 m 2 /g to about 5000 m 2 /g, about 150 m 2 /g to about 4000 m 2 /g, about 200 m 2 /g to about 1000 m 2 /g, about 500 m 2 /g to 1000 m 2 /g, about 1000 m 2 /g to about 2500 m 2 /g, about 2000 m 2 /g to about 3000 m 2 /g, about 100 m 2 /g to 500 m 2 /g, about 400 m 2 /g to about 500 m 2 /g, or any surface area in a range bounded by any of these values.
  • the graphene oxide may be platelets having 1, 2, or 3 dimensions with size of each dimension independently in the nanometer to micron range.
  • the graphene may have a platelet size in any one of the dimensions, or may have a square root of the area of the largest surface of the platelet, of about 0.05-100 ⁇ m, about 0.05-50 ⁇ m, about 0.1-50 ⁇ m, about 0.5-10 ⁇ m, about 1-5 ⁇ m, about 0.1-2 ⁇ m, about 1-3 ⁇ m, about 2-4 ⁇ m, about 3-5 ⁇ m, about 4-6 ⁇ m, about 5-7 ⁇ m, about 6-8 ⁇ m, about 7-10 ⁇ m, about 10-15 ⁇ m, about 15-20 ⁇ m, about 50-100 ⁇ m, about 60-80 ⁇ m, about 50-60 ⁇ m, about 25-50 ⁇ m, or any platelet size in a range bounded by any of these values.
  • the graphene material can comprise at least 70%, at least 75%, at least 80%, at least 85%, at least 90%, at least 95%, at least 97%, or at least 99% of graphene material having a molecular weight of about 5000 Daltons to about 200,000 Daltons.
  • the optionally substituted graphene oxide may be unsubstituted.
  • the optionally substituted graphene oxide may comprise a non-functionalized graphene base.
  • the graphene material may comprise a functionalized graphene base.
  • Functionalized graphene includes one or more functional groups not present in graphene oxide, such as functional groups that are not OH, COOH or epoxide group directly attached to a C-atom of the graphene base. Examples of functional groups that may be present in functionalized graphene include halogen, alkene, alkyne, CN, ester, amide, or amine.
  • Graphene oxide includes any graphene having epoxy substituents and saturated carbon atoms.
  • the graphene material such as optionally substituted graphene oxide, may comprise a functionalized graphene base.
  • more than: about 90%, about 80%, about 70%, about 60% about 50%, about 40%, about 30%, about 20%, or about 10% of the optionally substituted graphene oxide may be functionalized.
  • the majority of optionally substituted graphene oxide may be functionalized.
  • substantially all the optionally substituted graphene oxide may be functionalized.
  • the functionalized graphene oxide may comprise a graphene base and functional compound.
  • the graphene base can be graphene oxide (GO), reduced-graphene oxide (RGO), functionalized graphene oxide, functionalized and reduced-graphene oxide, or any combination thereof.
  • the functionalized graphene contains multiple types of functional groups in addition to at least one epoxide group. In some embodiments, there is only one type of functional groups in the functionalized graphene.
  • the epoxide groups can be the by-product of oxidation of the graphene to create graphene oxide. In some embodiments, the epoxide groups are formed on the surface of the graphene base by additional chemical reactions. In some embodiments, the epoxide groups are formed during oxidation and additional chemical reactions.
  • the mass percentage of the graphene base relative to the total composition of the graphene containing layer can be about 1 wt % to about 95 wt %, about 10 wt % to about 95 wt %, about 30 wt % to about 80 wt %, about 20-50 wt %, about 30-50 wt %, about 40-60 wt %, about 60-80 wt %, or 80-95 wt %.
  • the selectively permeable membrane can comprise crosslinked, optionally substituted graphene oxide.
  • the crosslinked, optionally substituted graphene oxide comprises a cross-linking group covalently bonding adjacent optionally substituted graphene oxides.
  • the optionally substituted graphene material may be a crosslinked graphene, where the graphene material may be crosslinked with at least one other graphene base by a cross-linker material/bridge. it is believed that crosslinking the graphene material can enhance the membrane's mechanical strength and water permeable properties by creating strong chemical bonding and wide channels between graphene platelets to allow water to pass through the platelets easily.
  • the graphene material may comprise crosslinked graphene material at the graphene bases having at least about 1%, about 5%, about 10%, about 20%, about 30%, about 40% about 50%, about 60%, about 70%, about 80%, about 90%, about 95%, or all of the graphene material crosslinked.
  • the majority of the graphene material may be crosslinked.
  • some of the graphene material may be crosslinked with at least 5% of the graphene material crosslinked with other graphene material. The amount of crosslinking may be estimated based on the weight of the cross-linker as compared with the total amount of graphene material.
  • one or more of the graphene base(s) that are crosslinked may also be functionalized.
  • the graphene material may comprise both crosslinked and non-crosslinked graphene, as well as crosslinked, functionalized, functionalized and non-crosslinked graphene.
  • the adjacent optionally substituted graphene oxides can be covalently bonded to each other by an optionally substituted phenylenediamine cross-linker.
  • the resulting cross-linked graphene oxide can be represented as following:
  • GO represents an optionally substituted graphene oxide and Ph represents an optionally substituted phenylene.
  • the phenylenediamine cross-linker is an optionally substituted meta-phenylenediamine as shown in Formula 2:
  • R is H, or an optionally substituted carboxylic acid.
  • the substituents can be Na, K, or Li.
  • R is H, CO 2 H, CO 2 Li, CO 2 Na, and/or CO 2 K.
  • the optionally substituted meta-phenylenediamine can be:
  • the cross-linker is a salt, such as sodium salt, potassium salt, or lithium salt
  • the hydrophilicity of the resulting GO membrane could be increased, thereby increasing the total water flux.
  • a cross-linkage containing two C—N bonds between optionally substituted graphene oxides can be generated by a ring opening reaction of an epoxide group in each of the optionally substituted graphene oxide with each of the 2 amine groups of a phenylene diamine cross-linker. Examples of the reactions are shown in Scheme 1 below where unsubstituted meta-phenylenediamine is used.
  • reaction between the optionally substituted meta-phenylenediamine and the optionally substituted graphene oxides can form a cross-linkage between two vertically stacked graphene oxides as represented in Scheme 2 below.
  • an optionally substituted phenylenediamine crosslinker such as substituted meta-phenylenediamine or unsubstituted meta-phenylenediamine crosslinks to a first interior carbon atom on a face of the first optionally substituted graphene oxide platelet and to a second interior carbon atom on a face of the second optionally substituted graphene oxide platelet.
  • An interior carbon atom on a face of an optionally substituted graphene oxide platelet is a carbon atom that is not on an outer border of the optionally substituted graphene oxide platelet.
  • crosslinks is interchangeable with the term “cross-links”.
  • an optionally substituted graphene oxide, crosslinked with a substituted phenylenediamine, such as a substituted m-phenylenediamine or an unsubstituted phenylenediamine, such as unsubstituted m-phenylenediamine can have about 5-60 atom %, about 5-10 atom %, about 10-15 atom %, about 15-20 atom %, about 15-25 atom %, about 20-40 atom %, about 20-25 atom %, about 30-35 atom %, about 40-60 atom %; at least: about 5 atom %, about 7 atom %, about 10 atom %, about 12 atom %, about 14 atom %, about 15 atom %, about 16 atom %, about 17 atom %, about 18 atom %, about 19 atom %, or about 20 atom %; about 21 atom %, about 34%, or about 33%; or any atom % of
  • an optionally substituted graphene oxide, crosslinked with a substituted phenylenediamine, such as a substituted m-phenylenediamine or an unsubstituted phenylenediamine, such as unsubstituted m-phenylenediamine can have about 20-90 atom %, about 30-80 atom %, about 40-75 atom %, about 60-75 atom %, about 60-70 atom %, about 50-70 atom %, about 60-65 atom %, about 68%, about 63% of carbon atom, or any atom % of carbon atom in a range bounded by any of these values.
  • the percentage of carbon atom can be determined by XPS.
  • an optionally substituted graphene oxide, crosslinked with a substituted phenylenediamine, such as a substituted m-phenylenediamine or an unsubstituted phenylenediamine, such as unsubstituted m-phenylenediamine can have a carbon to oxygen atom ratio (C/O) of about 1-5.5, about 1.5-5, about 1-5, about 1-4, about 1-3, about 2-5, about 2-4, about 2-3, about 1.6-4, about 1.7-3.5, about 1.8-3.3, about 3-4, about 3-3.5, about 1-2, about 1.5-2, about 3.2, or about 1.9, or any atom ratio of C/O in a range bounded by any of these values.
  • C/O carbon to oxygen atom ratio
  • an optionally substituted graphene oxide, crosslinked with a substituted phenylenediamine, such as a substituted m-phenylenediamine or an unsubstituted phenylenediamine, such as unsubstituted m-phenylenediamine can have less than about 20 atom %, less than about 15 atom %, less than about 13 atom %, less than 11.5 atom %, less than about 11 atom %, less than about 10 atom %, about 10-11 atom %, about 10.9 atom %, about 1-20 atom %, about 3-6 atom %, about 5-15 atom %, about 9-13 atom %, about 10-12 atom % of nitrogen, or any atom percent in a range bounded by any of these values.
  • the percentage of nitrogen atoms which may reflect the degree of crosslinking in GO-MPD membrane, can be determined by XPS.
  • an optionally substituted graphene oxide, crosslinked with a substituted phenylenediamine, such as a substituted m-phenylenediamine or an unsubstituted phenylenediamine, such as unsubstituted m-phenylenediamine can have an interlayer distance or d-spacing of about 0.5-3 nm, about 0.6-2 nm, about 0.7-1.7 nm, about 0.8-1.5 nm, about 0.9-1.5 nm, about 1.4-1.5 nm, about 0.9-1 nm, about 1.4 nm, about 1.43, about 0.9 nm, about 0.93 nm, or any distance in a range bounded by any of these values.
  • the d-spacing can be determined by x-ray powder diffraction (XRD).
  • the GO-MPD layer may have any suitable thickness.
  • some GO-MPD layers may have a thickness of about 5-200 nm, 10-100 nm, about 10-50 nm, about 10-20 nm, about 20-30 nm, about 30-40 nm, about 40-50 nm, about 50-70 nm, about 70-100 nm about 10 nm, 12 nm, about 20 nm, about 30 nm, about 40 nm, about 50 nm, about 60 nm, about 80 nm, about 100 nm, or any thickness in a range bounded by any of these values.
  • the fluid can comprise a liquid.
  • the fluid can comprise a gas.
  • the gas can comprise multiple gases including water vapor.
  • the method controls the concentration of water vapor in a gas.
  • the method controls the concentration of water in a liquid.
  • the fluid containing high concentration of water can be an unprocessed fluid.
  • the method can provide removal of water from the unprocessed fluid, or dehydration, to reach desired water concentrations of the unprocessed fluid; thereby to yield a processed fluid.
  • a method of dehydrating of an unprocessed fluid comprises contacting the unprocessed fluid to the one or more of the aforementioned membranes. In some embodiments, contacting the unprocessed fluid to the membrane can result in allowing the water to pass through the membrane to a second fluid, or effluent. In some embodiments, exposing the unprocessed fluid to the membrane further comprises allowing sufficient time for the water to pass through the membrane so that the processed fluid achieves the desired water concentration. In some embodiments, the unprocessed fluid is in a gaseous phase, wherein the water being removed is water vapor. In some embodiments, the unprocessed fluid is in the liquid phase, wherein the water being removed is liquid water.
  • the method comprises allowing water vapor to pass through the membrane. In some embodiments, the method comprises allowing liquid water to pass through the membrane. In some embodiments, the method comprises allowing a combination of water vapor and liquid water to pass through the membrane.
  • the desired water concentration can be a concentration (but not limited to), of water vapor content in an enclosed space that is below the level which would result in condensation, mold growth, and/or spoliation of food.
  • passing the water through the membrane can be by osmosis, or under the power of osmotic pressure.
  • the method further comprises providing a pressure gradient across the membrane to force the water passing through the membrane to overcome osmotic back pressure.
  • a method for removing a solute from an unprocessed solution can comprise contacting the unprocessed solution to one or more of the aforementioned membranes. In some embodiments, the method further comprises passing the solution through the membrane. In some embodiments, passing the water containing solute through the membrane can be accomplished by supplying a means of producing head pressure. In some embodiments, the head pressure can be sufficient to overcome osmotic back pressure. In some embodiments, the method comprises retaining the solutes by the membrane while allowing water to pass through, thereby reducing the solute content of the water. In some embodiments, the method can further comprise providing a pressure gradient across the membrane.
  • providing a pressure gradient across the membrane can be achieved by producing a positive pressure in the first reservoir, producing a negative pressure in the second reservoir, or producing a positive pressure in the first reservoir and producing a negative pressure in the second reservoir.
  • a means of producing a positive pressure in the first reservoir can be accomplished by using a piston, a pump, a gravity drop, and/or a hydraulic ram.
  • a means of producing a negative pressure in the second reservoir can be achieved by applying a vacuum or withdrawing fluid from the second reservoir.
  • Some embodiments include methods for making a membrane comprising: preparing solutions of graphene oxide and a cross-linker, applying the solutions to a substrate, and curing the mixture on a substrate.
  • a layer-by-layer method is used, wherein applying the solutions to the substrate comprises applying layer by layer of a plurality of alternating layers of graphene oxide and cross-linker to the substrate.
  • FIG. 6 A non-limiting example is shown in FIG. 6 .
  • a filtering method is used, wherein applying the solutions to the substrate comprises applying a single layer of a mixed graphene oxide and cross-linker solution and then filtering the resulting coating solution through the pretreated substrate.
  • FIG. 7 A non-limiting example is shown in FIG. 7 .
  • a mixture coating method is used, wherein applying a single layer or a plurality of layers of a mixed graphene oxide and cross-linker coating solution to the pretreated substrate to form one or a plurality of layers.
  • the graphene oxide comprises optionally substituted graphene oxide.
  • the cross-linker comprises optionally substituted meta-phenylenediamine.
  • the method of making a membrane comprises: (a) mixing an optionally substituted graphene oxide and a cross-linker to get an aqueous solution; (b) resting the solution for 30 minutes to 12 hours to create a coating mixture; (c) applying the coating mixture to a substrate; (d) repeating step (c) as necessary to achieve the desired thickness or number of layers; and (e) curing the optionally substituted graphene oxide and the cross-linker upon the substrate at 50° C. to 120° C. for 15 minutes to 2 hours so that the optionally substituted graphene oxide and the cross-linker are covalently bonded.
  • applying the coating mixture to the substrate can be achieved by immersing the substrate into the coating mixture first, and then drawing the solution onto the substrate by applying a negative pressure gradient across the substrate until the desired coating thickness can be achieved.
  • applying the coating mixture to the substrate can be achieved by blade coating, spray coating, dip coating, or spin coating.
  • the method can further comprise rinsing the substrate with deionized water after application of the coating mixture.
  • the method can further comprise applying a salt rejection layer.
  • Some embodiments include a method of making a membrane from an optionally substituted meta-phenylenediamine cross-linker and an optionally substituted graphene oxide comprising: (a) separately applying an optionally substituted graphene oxide aqueous solution and an optionally substituted meta-phenylenediamine cross-linker aqueous solution to a substrate; (b) repeating step (a) as necessary to achieve the desired thickness or number of layers; and (c) curing the optionally substituted graphene oxide and the cross-linker upon the substrate at 50-120° C. for 15 minutes to 2 hours so that the optionally substituted graphene oxide and optionally substituted meta-phenylenediamine cross-linker can covalently bond.
  • Applying the aqueous solutions to the substrate can be achieved by methods such as blade coating, spray coating, dip coating, spin coating, etc. Some methods can further comprise rinsing the substrate with deionized water after each application of either an optionally substituted meta-phenylenediamine cross-linker aqueous solution or an optionally substituted graphene oxide aqueous solution. In some embodiments, the method can further comprise applying a salt rejection layer.
  • the method comprises optionally pre-treating a substrate to assist in the adhesion of the graphene oxide to the substrate.
  • pretreating the substrate comprises treating the substrate with a dopamine solution.
  • the dopamine solution can be polymerized to form polydopamine on the substrate.
  • the method comprises drying the pretreated substrate at about 40-90° C. In some embodiments, the pretreated substrate can be dried at about 65° C.
  • the method comprises applying a graphene oxide aqueous solution and a cross-linker aqueous solution to the substrate.
  • applying a graphene oxide aqueous solution and a cross-linker aqueous solution to the substrate can be achieved by layer-by-layer method, filter method, or mixture coating method, which results a coated substrate.
  • the application procedure can be repeated until the desired thickness or number of layers of the graphene oxide and the cross-linker are achieved.
  • the thickness or number of layers is defined so that the resulting membrane meets the aforementioned membrane performance criteria.
  • the desired thickness of membrane can range from about 5-2000 nm, about 5-1000 nm, about 1000-2000 nm, about 10-500 nm, about 500-1000 nm, about 50-300 nm, about 10-200 nm, about 10-100 nm, about 10-50 nm, about 20-50 nm, or about 50-100.
  • the number of layers can range from 1 to 250, from 1 to 100, from 1 to 50, from 1 to 20, from 1 to 15, from 1 to 10, or from 1 to 5. This process results in a fully coated substrate.
  • the method further comprises heating the fully coated substrate to facilitate the crosslinking, or forming covalent bonding, of the graphene oxide and the cross-linker.
  • the fully coated substrate can be heated in an oven at about 50-120° C., about 40-150° C., about 50-100° C., about 80-90° C., about 40-60° C., about 120° C., about 50° C., or about 80° C. In some embodiments, the fully coated substrate can be heated for a period of about 15 minutes to about 2 hours, about 0.5-1 h, about 1 hour, or about 30 minutes to result a membrane.
  • the method for fabricating membranes further comprises applying a salt rejection layer to the membrane or a cured substrate to yield a membrane with a salt rejection layer.
  • the salt rejection layer can be applied by dipping the cured substrate into a solution of precursors in mixed solvents.
  • the precursors can comprise an amine and an acyl chloride.
  • the precursors can comprise meta-phenylenediamine and trimesoyl chloride.
  • the concentration of meta-phenylenediamine can range from about 0.01-10 wt %, about 0.1-5 wt %, about 5-10 wt %, about 1-5 wt %, about 2-4 wt %, about 4 wt %, about 2 wt %, or about 3 wt %.
  • the trimesoyl chloride concentration can range from about 0.001 vol % to about 1 vol %, about 0.01-1 vol %, about 0.1-0.5 vol %, about 0.1-0.3 vol %, about 0.2-0.3 vol %, about 0.1-0.2 vol %, or about 0.14 vol %.
  • the mixture of meta-phenylenediamine and trimesoyl chloride can be allowed to rest for a sufficient amount of time such that polymerization can take place before the dipping occurs.
  • the method comprises resting the mixture at room temperature for about 1-6 hours, about 5 hours, about 2 hours, or about 3 hours.
  • the method comprises dipping the cured substrate in the coating mixture for about 15 seconds to about 15 minutes; about 5 seconds to about 5 minutes, about 10 seconds to about 10 minutes, about 5-15 minutes, about 10-15 minutes, about 5-10 minutes, or about 10-15 seconds.
  • the salt rejection layer can be applied by coating the cured substrate in separate solutions of aqueous meta-phenylenediamine and a solution of trimesoyl chloride in an organic solvent.
  • the meta-phenylenediamine solution can have a concentration in a range of about 0.01-10 wt %, about 0.1-5 wt %, about 5-10 wt %, about 1-5 wt %, about 2-4 wt %, about 4 wt %, about 2 wt %, or about 3 wt %.
  • the trimesoyl chloride solution can have a concentration in a range of about 0.001-1 vol %, about 0.01-1 vol %, about 0.1-0.5 vol %, about 0.1-0.3 vol %, about 0.2-0.3 vol %, about 0.1-0.2 vol %, or about 0.14 vol %.
  • the method comprises dipping the cured substrate in the aqueous meta-phenylenediamine for a period of about 1 second to about 30 minutes, about 15 seconds to about 15 minutes; or about 10 seconds to about 10 minutes. In some embodiments, the method then comprises removing excess meta-phenylenediamine from the cured substrate.
  • the method then comprises dipping the cured substrate into the trimesoyl chloride solution for a period of about 30 seconds to about 10 minutes, about 45 seconds to about 2.5 minutes, or about 1 minute.
  • the method comprises subsequently drying the cured substrate in an oven to yield a membrane with a salt rejection layer.
  • the cured substrate can be dried at about 45° C. to about 200° C. for a period about 5 minutes to about 20 minutes, at about 75° C. to about 120° C. for a period of about 5 minutes to about 15 minutes, or at about 90° C. for about 10 minutes. This process results in a membrane with a salt rejection layer.
  • the method for fabricating a membrane further comprises subsequently applying a protective coating on the membrane.
  • the applying a protective coating comprises adding a hydrophilic polymer layer.
  • applying a protective coating comprises coating the membrane with a PVA aqueous solution. Applying a protective layer can be achieved by methods such as blade coating, spray coating, dip coating, spin coating, and etc.
  • applying a protective layer can be achieved by dip coating of the membrane in a protective coating solution for about 1 minute to about 10 minutes, about 1-5 minutes, about 5 minutes, or about 2 minutes.
  • the method further comprises drying the membrane at a about 75° C. to about 120° C. for about 5 minutes to about 15 minutes, or at about 90° C. for about 10 minutes. This results in a membrane with a protective coating.
  • a layer-by-layer method is used to apply a graphene oxide aqueous solution and a cross-linker aqueous solution, such as an optionally substituted meta-phenylenediamine, to a substrate, wherein the method comprises applying the aforementioned solutions separately layer by layer to form a plurality of layers.
  • the number of layers can range from 1-100, 1-50, 1-20, 1-15, 1-10, or 1-5, or is 10, wherein a coating of graphene oxide and a coating of optionally substituted meta-phenylenediamine cross-linker is considered a single layer.
  • the aqueous graphene oxide solution can have a concentration ranging from about 0.0001-0.01 wt %.
  • the optionally substituted meta-phenylenediamine cross-linker aqueous solution can have a concentration ranging from 0.0001-0.01 wt %.
  • applying the optionally substituted meta-phenylenediamine cross-linker aqueous solution can be followed by applying the graphene oxide aqueous solution.
  • applying the graphene oxide aqueous solution can be followed by applying the optionally substituted meta-phenylenediamine cross-linker aqueous solution.
  • applying the aqueous solutions can be achieved independently by blade coating, spray coating, dip coating, spin coating, or other methods known in the art. In some embodiments, applying the solutions can be done by dip coating the substrate in the respective solution for about 1 minute to about 10 minutes, about 1-5 minutes, or about 5 minutes.
  • the layer-by-layer method further comprises rinsing the resulting substrate in deionized (DI) water to remove excess material after the application of either the graphene oxide aqueous solution and/or the optionally substituted meta-phenylenediamine cross-linker aqueous solution to yield a coated substrate.
  • DI deionized
  • a filtering method is used to apply a graphene oxide aqueous solution and a cross-linker aqueous solution to a substrate, wherein the method comprises creating a mixed coating solution, resting the coating solution to form a coating mixture, and then filtering the coating mixture through the substrate to generate a coated substrate.
  • creating a mixed coating solution comprises preparing a single mixed coating solution by mixing aqueous solutions of a graphene oxide and a cross-linker. In some embodiments, creating a mixed coating solution comprises mixing the graphene oxide aqueous solution with a concentration of about 0.0001-0.01 wt %, and the cross-linker aqueous solution with a concentration of about 0.0001-0.01 wt % to yield a coating solution.
  • the filtering method comprises resting the coating solution at about room temperature for a period of about 30 minutes to about 12 hours, about 1-6 hours, about 2-5 hours, 2-4 hours, about 5 hours, or about 3 hours. It is believed that resting the coating solution could allow the graphene oxide and the cross-linker to begin covalently bonding to facilitate the generation of a final crosslinked layer.
  • the filtering method comprises immersing the substrate in the coating mixture. In some embodiments, the method further comprises drawing the coating mixture into the substrate by applying a negative pressure gradient across the substrate.
  • the negative pressure gradient can be applied through a vacuum on one side of the substrate.
  • the duration of the drawing of the mixture can be varied such that a desired total thickness of the resulting coating layer is achieved, e.g., about 10-100 nm, about 10-50 nm, about 10 nm, 12 nm, about 20 nm, about 30 nm, about 40 nm, about 50 nm, or about 100 nm.
  • the filtering method further comprises rinsing the resulting substrate with deionized (DI) water to remove excess material after application of the coating mixture to yield a coated substrate.
  • DI deionized
  • a mixture coating method is used to apply a graphene oxide aqueous solution and a cross-linker aqueous solution to a substrate, wherein the method comprises creating a mixed coating solution, resting the coating solution to form a coating mixture, and then applying the coating mixture to form a plurality of layers on the substrate.
  • the number of layers can range from 1 to about 100, where a single mixed layer in considered a single layer.
  • creating a mixed coating solution comprises creating a single mixed coating solution by mixing aqueous solutions of a graphene oxide and a cross-linker. In some embodiments, creating a mixed coating solution comprises mixing the graphene oxide solution with concentration of about 0.0001-0.01 wt % and the cross-linker aqueous solution with concentration of about 0.0001-0.01 wt % to yield a coating solution.
  • the mixture coating method comprises resting the coating solution at about room temperature for about 30 minutes to about 12 hours, about 1-6 hours, about 5 hours, or about 3 hours. It is believed that resting the coating solution allows the graphene oxide and the cross-linker to begin covalently bonding to facilitate the generation of a final crosslinked layer.
  • the mixture coating method further comprises applying the coating mixture to the substrate.
  • applying a coating mixture to the substrate can be accomplished by blade coating, spray coating, dip coating, spin coating, or other methods known in the art.
  • applying a coating mixture can be achieved by spray coating the substrate.
  • the mixture coating method optionally comprises rinsing the resulting substrate with DI water after application of the coating mixture to remove excess materials, which yields a coated substrate.
  • a membrane comprising:
  • a graphene oxide layer comprising an optionally substituted cross-linked graphene oxide in fluid communication with the porous substrate;
  • optionally substituted cross-linked graphene oxide comprises an optionally substituted graphene oxide and a cross-linkage represented by Formula 1:
  • R is H, CO 2 H, CO 2 Li, CO 2 Na, or CO 2 K.
  • the membrane of embodiment 1, 2, or 3, wherein the optionally substituted graphene oxide comprises platelets.
  • the membrane of embodiment 1, 2, 3, 4, or 5, wherein the optionally substituted cross-linked graphene oxide material is about 1 atom % to about 20 atom % nitrogen.
  • the membrane of embodiment 1, 2, 3, 4, or 5, wherein the optionally substituted cross-linked graphene oxide material is about 3 atom % to about 6 atom % nitrogen.
  • the membrane of embodiment 1, 2, 3, 4, or 5, wherein the optionally substituted cross-linked graphene oxide material is about 5 atom % to about 15 atom % nitrogen.
  • the membrane of embodiment 1, 2, 3, 4, or 5, wherein the optionally substituted cross-linked graphene oxide material is about 9 atom % to about 13 atom % nitrogen.
  • the membrane of embodiment 1, 2, 3, 4, or 5, wherein the optionally substituted cross-linked graphene oxide material is about 10 atom % to about 12 atom % nitrogen.
  • the membrane of embodiment 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, or 11, wherein the optionally substituted cross-linked graphene oxide is prepared by reacting an optionally substituted meta-phenylenediamine (MPD) with an optionally substituted graphene oxide (GO), wherein the weight ratio of optionally substituted meta-phenylenediamine to optionally substituted graphene oxide (MPD/GO) is in a range of about 0.1 to about 100.
  • MPD meta-phenylenediamine
  • GO optionally substituted graphene oxide
  • MPD/GO optionally substituted graphene oxide
  • the membrane of embodiment 12, wherein the weight ratio of optionally substituted meta-phenylenediamine to optionally substituted graphene oxide (MPD/GO) is in a range of 1 to 10.
  • the membrane of embodiment 13, wherein the weight ratio of optionally substituted meta-phenylenediamine to optionally substituted graphene oxide (MPD/GO) is about 1, about 3, or about 7.
  • the membrane of embodiment 13, wherein the weight ratio of optionally substituted meta-phenylenediamine to optionally substituted graphene oxide (MPD/GO) is about 3, or about 7.
  • the membrane of embodiment 13, wherein the weight ratio of optionally substituted meta-phenylenediamine to optionally substituted graphene oxide (MPD/GO) is about 7.
  • the membrane of embodiment 18 or 19, wherein the salt rejection layer comprises a polyamide prepared by reacting a meta-phenylenediamine with trimesoyl chloride.
  • the thickness of the graphene oxide layer is about 10 nm to about 100 nm.
  • the membrane of embodiment 19, comprising 1 layer to 10 layers of coating of GO and MPD.
  • a method for dehydrating an unprocessed fluid comprising exposing the unprocessed fluid to the membrane of embodiment 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, or 25.
  • a method for removing a solute from an unprocessed solution comprising exposing the unprocessed solution to the membrane of embodiment 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, or 25.
  • a method of making a membrane comprising:
  • the applying the coating mixture to the substrate comprises immersing the substrate into the coating mixture and then drawing the coating mixture into the substrate by applying a negative pressure gradient across the substrate until the desired coating thickness is achieved.
  • the method of embodiment 30, wherein the applying the coating mixture to the substrate comprises blade coating, spray coating, dip coating, or spin coating.
  • a method of making a membrane from an optionally substituted meta-phenylenediamine cross-linker and an optionally substituted graphene oxide comprising:
  • step (a) is achieved by blade coating, spray coating, dip coating, or spin coating of one or both of the aqueous solutions.
  • the salt rejection layer comprises a polyamide prepared by a method comprising reacting a meta-phenylenediamine with trimesoyl chloride.
  • GO was prepared from graphite using the modified Hummers method.
  • Graphite flakes 2.0 g (Sigma Aldrich, St. Louis, Mo., USA, 100 mesh) were oxidized in a mixture of 2.0 g of NaNO 3 (Aldrich), 10 g KMnO 4 of (Aldrich) and 96 mL of concentrated H 2 SO 4 (Aldrich, 98%) at 50° C. for 15 hours.
  • the resulting paste like mixture was poured into 400 g of ice followed by adding 30 mL of hydrogen peroxide (Aldrich, 30%). The resulting solution was then stirred at room temperature for 2 hours to reduce the manganese dioxide, then filtered through a filter paper and washed with DI water.
  • the solid was collected and then dispersed in DI water with stirring, centrifuged at 6300 rpm for 40 minutes, and the aqueous layer was decanted. The remaining solid was then dispersed in DI water again and the washing process was repeated 4 times.
  • the purified GO was then dispersed in DI water under sonication (power of 20 W) for 2.5 hours to get the GO dispersion (0.4 wt %) as GC-1.
  • the dopamine was polymerized to form polydopamine on the substrate.
  • the polydopamine-coated substrate was dried in oven (DX400, Yamato Scientific Co., Ltd. Tokyo, Japan) at 65° C. This process resulted in a pre-treated substrate.
  • GO dispersion GC-1
  • DI water DI water
  • a 0.1 wt % of meta-phenylenediamine (MPD) aqueous solution was prepared by dissolving an appropriate amount of MPD (Aldrich) in DI water.
  • MPD meta-phenylenediamine
  • a coating mixture was created by dissolving the aqueous solutions of 0.1 wt % MPD and 0.1 wt % GO in DI water at a weight ratio of 1:1.
  • the resulting solution was then rested for about 3 hours, or normally until the GO and amine have finished reacting.
  • the resulting coating mixture was then filtered through the pretreated substrate under vacuum to draw the solution through the substrate.
  • MD-1.1.1.1.2 through MD-1.1.2.1.4 were constructed using the methods similar to Example 2.1.1, with the exception that parameters were varied for the specific membranes as shown in Table 1.
  • the substrate e.g., polysulfone (PSF), polyether sulfone (PES), polyamide (Nylon), polyimide (PI), or polyvinylidene fluoride (PVDF)
  • layer thickness e.g., layer thickness, cross-linker [e.g., MPD or 3, 5-diaminobenzoic acid (MPD w/COOH) (Aldrich)], and mass ratio of cross-linker to GO were varied.
  • PSF polysulfone
  • PES polyether sulfone
  • PI polyimide
  • PVDF polyvinylidene fluoride
  • layer thickness e.g., MPD or 3, 5-diaminobenzoic acid (MPD w/COOH) (Aldrich)
  • the GO preparation and substrate preparation can use the same method as that in Example 2.1.1 with the exception of the GO-MPD preparation method, which varies as described below.
  • the GO dispersion, GC-1 can be diluted with DI water to create a 0.1 wt % GO aqueous solution.
  • a 0.1 wt % MPD aqueous solution can be prepared by dissolving an appropriate amount of MPD (Aldrich) in DI water.
  • a coating solution can be created by dissolving the aqueous solutions of 0.1 wt % GO and 0.1% MPD in DI water at a weight ratio of 1:1.
  • the resulting coating solution can be rested for about 3 hours, or normally until the GO and the amine have beenpre-reacted. This process can result in a coating mixture.
  • the polydopamine-coated substrate can be then coated with the above described coating mixture by dipping the substrate in the coating mixture.
  • the substrate can be rinsed thoroughly in DI water to remove any excess particles.
  • the aforementioned process can be repeated, that is dipping the substrate into the coating mixture and then rinsing with DI water for a number of cycles to get the desired number of layers or thickness of GO and MPD.
  • the resulting membrane can be then kept in an oven (DX400, Yamato Scientific) at 80° C. for 30 minutes to facilitate further crosslinking. This process can result in a membrane without a salt rejection layer.
  • Example 2.1.3 Preparation of a Membrane Via Layer-by-Layer Application (MD-1.3.1.1.1)
  • the GO preparation and substrate preparation used the same method as that in Example 2.1.1 with the exception that the GO-MPD application method varied as described below and polysulfone (PSF) was used as a substrate.
  • PSF polysulfone
  • a 0.1 wt % MPD aqueous solution was prepared by dissolving an appropriate amount of MPD (Aldrich) in DI water.
  • a 0.1 wt % GO aqueous solution was made by diluting the GO dispersion, GC-1 in DI water.
  • the polydopamine-coated substrate was then soaked in 0.1 wt % MPD aqueous solution for 5 minutes, rinsed thoroughly with DI water, and subsequently soaked in 0.1 wt % GO solution for 5 minutes to attach the first layer of GO. Next, the membrane was rinsed with DI water to remove excess GO.
  • This process can be repeated, alternately dipping the substrate into MPD and GO solution, for a number of cycles to get the desired number of layers of GO and MPD.
  • the membrane with one layer was prepared.
  • the resulting membrane was then kept in an oven (DX400, Yamato Scientific) at 80° C. for 30 minutes to facilitate further crosslinking. This process resulted in a membrane without a salt rejection layer (MD-1.3.1.1.1).
  • MD-1.1.1.1.1 was additionally coated with a polyamide salt rejection layer.
  • a 3.0 wt % MPD aqueous solution was prepared by diluting an appropriate amount of MPD (Aldrich) in DI water.
  • a 0.14 vol % trimesoyl chloride solution was made by diluting an appropriate amount of trimesoyl chloride (Aldrich) in isoparrifin solvent (Isopar E & G, Exxon Mobil Chemical, Houston Tex., USA).
  • the GO-MPD coated membrane was then dipped in the aqueous solution of 3.0 wt % of MPD (Aldrich) for a period of 10 seconds to 10 minutes depending on the substrate and then removed.
  • Example 2.2.1.1 Addition of a Salt Rejection Layer to Additional Membranes
  • Example 2.2.2 Preparation of a Membrane with a Protective Coating
  • This coating was made by known methods in the art.
  • a PVA solution of 2.0 wt % can be prepared by stirring 20 g of PVA (Aldrich) in 1 L of DI water at 90° C. for 20 minutes until all granules dissolve. The solution was then cooled to room temperature. The selected substrates can be immersed in the solution for 10 minutes and then removed. Excess solution remaining on the membrane can then be removed by paper wipes. The resulting assembly can then be dried in an oven (DX400, Yamato Scientific) at 90° C. for 30 minutes. A membrane with a protective coating can thus be obtained.
  • CMDs Comparative membranes
  • CMD-1.1 through CMD-1.2 were created using commercially available substrate components of polysulfone membrane (PSF) (Sterlitech Corporation, Kent, Wash., USA) and polypropolyene (PP) filtration membrane (Celgard LLC, Charlotte, N.C., USA).
  • PSF polysulfone membrane
  • PP polypropolyene
  • CMD-1.3 a PVA/PP membrane, was created by immersing a PP filtration membrane in a PVA/water solution (Aldrich) for 10 minutes and then drying the resulting membrane in an oven (DX400, Yamato Scientific) at 90° C. for about 30 minutes.
  • Comparative membranes CMD-2.1.1 through CMD-2.2.2 were made using methods similar to those used in Example 2.1.1 with the variations outlined in Table 3.
  • Membrane MD-1.1.1.1.1 was analyzed with a Transmission Electron Microscope (TEM). The TEM procedures are similar to those known in the art. The TEM cross-section analysis of GO-MPD membrane is shown in FIG. 9 .
  • the membrane thickness is about 5-10 nm, and is continuous along the substrate.
  • Membrane MD-1.1.1.1.1 was analyzed by X-ray photoelectron spectroscopy (XPS) to determine the relative distribution of the atomic spectra.
  • XPS X-ray photoelectron spectroscopy
  • Table 4 The XPS analysis, shown in Table 4, indicates a significant increase of nitrogen in the GO-MPD membrane, due to the cross-linking of MPD with GO, and partial reduction of oxygen as the epoxide was significantly reduced.
  • the basic GO-MPD membrane structure in a representative MD-1.1.1.1.1 membrane was characterized by X-ray Diffraction (XRD) as shown in FIG. 10 .
  • the structure was the same as MD-1.1.1.1.1 except that the substrate was a nylon substrate to facilitate testing.
  • IR analysis of GO-MPD structure in the MD-1.1.1.1.1 membrane was performed using methods known in the art.
  • the IR analysis as shown in FIG. 11 for both GO and GO-MPD indicating the formation of C—N and N—H bonds.
  • the existence of the C—N and N—H bonds suggests that cross-linking has occurred.
  • the water vapor permeability of the membranes was tested.
  • Nitrogen was chosen to mimic air.
  • FIG. 12 A sample diagram of the setup is shown in FIG. 12 .
  • the test setup consisted of a cross-flow test cell (CF016A, Sterlitech) which forms two plenums on either side, each with its own inlet and an outlet.
  • the membrane being measured was placed in the 45 mm ⁇ 45 mm testing chamber and sandwiched between the two halves of the test cell to create two sealed plenums when the shells are mated, each plenum in fluid communication only through the membrane. Then the inlets and outlets were chosen such that the fluid flow in each plenum was in a counter-flow configuration.
  • the wet N 2 gas was sent into the setup from the wet side, the first side, and then exited with some residual water vapor and gas permeated from the membrane sample into the second side, the dry side.
  • the sweep or dry N 2 gas was sent into the setup and then vented, with the wet gas being entrained from the membrane.
  • Humidity and Temperature were measured at three positions: input and output on the wet N 2 gas side, and output on the dry N 2 gas side using a Humidity/Temperature Transmitters (RHXL3SD, Omega Engineering, Inc., Stamford, Conn., USA).
  • the flow rate was also measured for both wet and dry sides by two Air Flow Sensors (FLR1204-D, Omega).
  • the gas pressure was also measured on both the wet and dry side by two Digital Pressure Gauges (Media Gauge MGA-30-A-9V-R, SSI Technologies, Inc., Janesville, Wis., USA).
  • the wet side inlet was set to a relative humidity of between about 80% to about 90%.
  • the dry side inlet had a relative humidity of 0%.
  • the upstream pressure for the wet gas stream was set to 0.13 psig.
  • the upstream pressure for the dry gas stream was set to 0.03 psig.
  • From the instruments the water vapor pressure and absolute humidity at the three measurement stations were derived/calculated from the measured temperature and humidity data. Then the water vapor transmission rate was derived from the difference in absolute humidity, flow rate, and exposed area of the membrane. Lastly, the water vapor permeability was derived from the water vapor transmission rate and the water vapor pressure difference between the two plenums.
  • the nitrogen flow rate was derived from the dry N 2 output and the wet N 2 inputs as well as the water vapor transmission rate.
  • a 0.5 mL manual bubble flow meter was used (#23771, Aldrich), which has a range of about 0.03 cc/min to about 5 cc/min, to determine the leakage rate instead of using the flow measurement instrument described above.
  • the selected membranes were placed in the setup and the wet side inlet was set to a relative humidity of between about 80% to about 90%.
  • the dry side inlet was closed to seal off the portion upstream of the flow measurement instrument so that only gas leaked through the membrane would go to the flow measurement instrument.
  • the upstream pressure for the wet gas stream was set to 0.13 psig and the leakage of the N 2 through the membrane was measured.
  • water permeability can be maintained by using larger substrate pores. Additionally, for the larger substrates, the effect of defects due to the large pore sizes can be minimized by increasing the GO-MPD layer thickness resulting in high water vapor permeability with the exclusion of other gases.
  • the GO-MPD coated PP substrates exhibited a distinct drop in permeability of other gases such as N 2 besides water when the thickness was above 16 nm. Additionally, the water vapor permeability remains at least 50% of that of the uncoated substrates (CMD-1.2 or CMD-1.3 membrane) demonstrating the ability of the membrane to reject other gases while maintaining water vapor flux across the membrane.
  • the reverse osmosis membrane comprising a 10-layer GO-MPD coated substrate (MD-2.3.1.1.3) was first tested to determine the membrane's ability to reject salt and retain adequate water flux. As seen in Table 10, the membrane has demonstrated high NaCl salt rejection and good water flux.
  • the salt rejection capability of membranes with various cross-linkers were also tested to determine the effect of different cross-linker materials and compared to the comparative examples to determine the relative effect of the new cross-linker materials.

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